Esterification kinetics on acetic acid
with isopropyl alcohol was studied in an intensified fixed bed reactor
at 333–353 K with Amberlyst 36 Wet. The effects of volume flow
rate, molar ratio of reactants, catalyst loading, and operating temperature
were investigated and optimized. The method of UNIFAC was applied
to calculate the activity coefficient of each component for correcting
the nonideality of the solution. Reaction enthalpy, entropy, and Gibbs
free energy were calculated in different cases. The pseudohomogeneous
model, Eley–Rideal model, and Langmuir–Hinshelwood–Hougen–Watson
model were used to establish kinetic equations of the reaction conducted
in the IFBR. It was proved that the LHHW model can accurately describe
the esterification kinetics in the intensified fixed bed reactor.